Carbon-caffeine separation

Description

Technical field

[0001] The present invention relates to decaffeination, and particularly to an improved process for recovering caffeine from an activated carbon adsorbent.

[0002] The decaffeination of vegetable materials and vegetable material extracts is of major commercial importance. Also significant is the recovery and sale of the caffeine removed from vegetable sources such as coffee and tea. It is known that activated carbon is a good adsorbent in caffeine recovery and purification procedures, but the carbon tends to hold the caffeine so tenaciously that, often, significant quantities of caffeine are lost or reduced in commercial value. None of the techniques currently available to the art for separating the caffeine from the carbon has been wholly satisfactory in terms of both degree and quality of caffeine recovery.

Background art

[0003] The recovery of caffeine from decaffeinating solvents has been an active area of concern for many years. For example, in U.S. 2,508,545, Shuman discloses that activated carbon and other adsorbents had been used to remove impurities from solutions of caffeine extracted from coffee. Shuman indicates that until the time of his invention caffeine losses due to adsorption onto the carbon ran as high as 10 to 14%. To rectify this, Shuman disclosed alternate use of organic and aqueous extractions with the final aqueous extraction being done at a pH of at least 7. While activated carbon is employed to remove impurities from the aqueous extract, the amounts employed are apparently small and no mention of separating caffeine from the carbon is made. Similarly, in U.S. 2,472,881, Bender employs activated carbon to remove impurities from an aqueous caffeine solution but does not discuss the steps taken to recover the caffeine adsorbed on the carbon.

[0004] DDR Patentschrift 78,586 relates to the recovery of caffeine from caffeine-containing active carbon with a solution of an aqueous acid (including acetic acid) of 5to 15%, preferably 7 to 10%, concentration and thereafter neutralizing the extraction solution and precipitating the caffeine cold. There is no suggestion that more efficient recovery of caffeine could be obtained using glacial acetic acid and other acids, alcohols, or azeotropes disclosed herein. Another reference, Chemical Abstract, volume 54: 12720 f-h ( 1960) discloses the desorption of caffeine from caffeine-containing activated carbon using chlorinated solvents and an ethanol solution of ammonia; these solvents are not food-grade as defined and required by the present invention.

[0005] Less relevant teachings are found in U.S. patent 2,391,981 which shows the use of non-chlorinated organic solvents and mixtures of solvents to desorb caffeine from coffee beans, clays or earths. German OS 2,716,798 makes no specific mention of caffeine recovery, but is a general reference suggesting that adsorbates can be desorbed from adsorbents, including activated carbon, using organic solvents such as methanol and isopropanol.

[0006] Recently, an improved decaffeination method was disclosed in U.S. 3,879,569 wherein quantitative extraction of caffeine from raw coffee beans is achieved with moist super-critical carbon dioxide. This process produces an extract from which essentially all of the caffeine can be removed by activated carbon. Unfortunately, the prior art techniques do not economically provide good levels of recovery of caffeine or they require the use of chlorinated hydrocarbon solvents which are otherwise avoided by the use of carbon dioxide as an extractant.

Disclosure of the invention

[0007] The present invention now enables improved recovery of caffeine from an activated carbon adsorbant, by a process comprising contacting activated carbon having caffeine obtained from decaffeination of vegetable material adsorbed thereon with a liquid, edible, non-toxic, food-grade caffeine solvent which consists essentially of an organic acid selectid form glacial acetic acid, propionic acid, or butyric acid or an alcohol selected from ethanol, isopropanol, benzyl alcohol, butanol, or amyl alcohol, or an azeotrope comprising at least one of these, and which solvent is capable of displacing at least a portion of the caffeine from active sites on the carbon; maintaining the contact for a period of time and at a temperature effective for the solvent to displace at least a portion of the caffeine from the carbon and dissolve the displaced caffeine; and separating caffeine from the solvent.

[0008] The present invention takes advantage of the discovery that some liquid, food-grade caffeine solvents which have the ability to effect desorption both by their strong solvent ability and their ability to displace the adsorbed material from active sites on the adsorbent, are extremely effective in separating caffeine from carbon adsorbents. The strong solvent effect causes a partitioning between the activated carbon and the solvent. The site displacement effect is achieved by the solvent molecules themselves competing for the active adsorbent sites. Once a caffeine molecule is displaced, it is then taken into solution by the solvent which is a strong solvent for caffeine.

[0009] The solvents employed according to the present invention are employed in their liquid state and preferably at temperatures in excess of 100°C to obtain the greatest rates of recovery. Temperature has a strong effect on desorption and should therefore be as high as possible, consistent with maintaining the solvent as a liquid. Where temperatures higher than the boiling point of the solvent are desired, it will be necessary to employ pressures in excess of atmospheric. It is preferred, however, to maintain the pressure at no greater than about atmospheric. Therefore, the higher boiling solvents are preferred.

[0010] Because the caffeine is valuable for food and pharmaceutical use, the solvents must be food-grade. By this, it is meant that the materials are on the Generally Recognized As Safe (GRAS) list maintained by the Food and Drug Administration to this type of use. This is important because where any measurable quantity of a non-GRAS material works its way into either the product caffeine or the product tea or coffee, the value of the product will be seriously diminished, if not wholly lost.

[0011] The organic acids and alcohols which are food-grade, liquid at the proposed processing temperature and preferably at room temperature, excellent solvents for caffeine, and capable of displacing caffeine from the active sites on the carbon, are effective solvents for use according to the invention. Thus, the solvent will comprise a member selected from the group consisting of glacial acetic acid, propionic acid, butyric acid, ethanol, isopropanol, benzyl alcohol, butanol, amyl alcohol, and azeotropes comprising at least one of these. Among the co-solvents which can be employed in forming the azeotropes are n-hexane, n-heptane, n-octane, toluene, benzyl acetate, methylene chloride, ethyl acetate and other food-grade solvents. The preferred solvents are those which have boiling points over 100°C, and of these glacial acetic acid and acetic acid azeotropes are the most preferred. The azeotropes of acetic acid with butyl alcohol, iso-amyl alcohol, toluene, and n-octane all have boiling points above 100°C as can be seen from the following table:

[0012] Other azeotropes suitable for use in the process of the invention, but requiring the use of superatmospheric pressures when temperatures of 100°C or more are employed, are:

[0013] Based on economy, effect on final product quality and effectiveness, glacial acetic acid is the most preferred of all the solvents.

[0014] The solvent is maintained in contact with the carbon having caffeine adsorbed thereon for a period of time and at a temperature effective for the solvent to displace at least a portion of the caffeine from the carbon and dissolve the displaced caffeine. As noted above, preferred temperatures will be above 100°C, but the specific temperature for any particular process will be selected on its own set of economic considerations and may be below this. Practical contact times will be determined on the basis of the desired degree of recovery and the desorption rate for a particular system. Preferably, the contact time should be sufficient to permit displacement of at least 75% by weight of the caffeine from the carbon and into solution with the solvent. Because the caffeine is valuable as a product and, if not removed from the carbon, decreases the adsorbent capacity of the carbon, still higher rates of displacement, on the order of 90% by weight or more, are desired.

[0015] As the activated carbon adsorbent can be any of those types commercially available which are effective caffeine adsorbents and capable of withstanding the rigors of recycling permitted by the invention. Preferred activated carbons are those prepared from coconut, coal and lignite, particularly those available commercially from Calgon Corporation, ICI, Carborundum and Union Carbide Corporation.

[0016] After contact for the requisite period of time, the activated carbon is preferably separated from the solvent prior to separation of the caffeine from the solvent. The simplest and most effective manner for removing the carbon from the solvent is by filtration.

[0017] The caffeine can be separated from the solvent in any suitable manner such as steam distillation or simply evaporating the solvent. In a preferred form of recovery, steam is passed through the caffeine-containing solvent in a vented vessel until the solvent concentration is reduced to about zero, most preferably about <1 ppm, leaving an aqueous caffeine solution. The caffeine is then precipitated from the aqueous solution by cooling to form pure white needle-shaped crystals.

Best mode for carrying out the invention

[0018] The following examples are for the purpose of illustrating and explaining the best mode for carrying out the invention, but are not meant to be limiting in any regard. Unless otherwise indicated, all parts and percentages are by weight.

Example 1

[0019] One hundred parts of glacial acetic acid and 10 parts of activated carbon pellets containing 10% by weight caffeine, obtained from the process of U.S. 3,879,569, were admixed and then refluxed in a vessel at atmospheric pressure and 117°C for two hours. The acetic acid as decanted from the carbon and found to contain 0.801 % caffeine. The carbon had 9.5 parts of acetic acid remaining on it. The caffeine was recovered from the solution by evaporation. The total amount of caffeine in the acetic acid was 0.725 parts, nearly 73% recovery in a single stage.

Example 2

[0020] The procedure of Example 1 was repeated but this time the components were introduced into a Soxhlet extraction tube and refluxed at 117°C for four hours. Total recovery of caffeine based on the 10% initial caffeine was 99%.

Example 3

[0021] The procedure of Example 2 was repeated, but this time employing a solvent containing 57 parts of n-butyl alcohol and 43 parts of glacial acetic acid. Afterfour hours contact at 120°C, 82% of the caffeine was recovered. On evaporation, white crystals of caffeine precipitated from the solution.

Example 4

[0022] In this example, green coffee beans are contacted with methylene chloride solvent to obtain a caffeine extract as described in U.S. 3,671,263. The solvent is removed from the extract by evaporation, leaving a brown, crude caffeine sludge containing large amounts of impurities in addition to caffeine. The sludge is preliminarily dissolved in water. Then the caffeine extract is contacted with DARCO powdered activated carbon which adsorbs most of the impurities from the extract to prepare it for crystallization into pure, white caffeine crystals. The carbon picks up about 10% caffeine in addition to the impurities. The caffeine is removed from the carbon by contacting the charcoal with glacial acetic acid for 4 hours at 100°C in a vessel. The carbon is separated from the acetic acid solution by filtration and the acid is evaporated to leave relatively pure crystals of caffeine. The acetic acid is condensed and recycled. The carbon is regenerated for recycle by thermal reactivation.

[0023] The above description has been for the purpose of teaching a person skilled in the art how to practice the invention. It is not intended to describe in detail each and every modification and variation of the invention which will become apparent to those skilled in the art upon study.

Claims

1. A process for recovering caffeine from activated carbon comprising: contacting activated carbon having caffeine obtained from decaffeination of vegetable material adsorbed thereon with a liquid, edible, non-toxic, food-grade caffeine solvent which consists essentially of an organic acid selected from glacial acetic acid, propionic acid, or butyric acid or an alcohol selected from ethanol, isopropanol, benzyl alcohol, butanol, or amyl alcohol, or an azeotrope comprising at least one of these, and which solvent is capable of displacing at least a portion of the caffeine from active sites on the carbon; maintaining the contact for a period of time and at a temperature effective for the solvent to displace at least a portion of the caffeine from the carbon and dissolve the displaced caffeine; and separating caffeine from the solvent.

2. A process according to claim 1 wherein the contact is maintained at a temperature in excess of 100°C.

3. A process according to either of claims 1 and 2 wherein the contact is maintained at a pressure in excess of atmospheric.

4. A process according to any one of claims 1 and 2 wherein the contact is maintained at a pressure of no greater than atmospheric.

5. A process according to any one of claims 2 to 4 wherein the solvent is glacial acetic acid or an acetic acid azeotrope containing a co-solvent selected from butyl alcohol, iso-amyl alcohol, toluene, n-hexane, n-heptane and n-octane.

6. A process according to any one of claims 1 to 5 wherein contact is maintained for a period of time sufficient to permit displacement of at least 75% by weight of the caffeine from the carbon and into solution with the solvent.

7. A process according to any one of claims 1 to 6 wherein the solvent is separated from the carbon by filtration prior to separating the caffeine from the solvent.

8. A process according to any one of claims 1 to 7 wherein the caffeine is separated from the solvent by steam distillation.

9. A process according to any one of claims 1 to 8 wherein the caffeine is separated from the solvent by evaporating the solvent.

Ansprüche

1. Verfahren zum Rückgewinnen von durch Entkoffeinieren von pflanzlichem Gut gewonnenen Koffein aus Aktivkohle, dadurch gekennzeichnet, daß adsorbiertes Koffein enthaltende Aktivkohle mit einem flüssigen, genießbaren, nichttoxischen, lebensmittelechten Koffeinlösungsmittel in Berührung gebracht wird, das im wesentlichen ausschließlich aus einer organischen Säure der Klasse Eisenessig, Propionsäure, Buttersäure oder aus einem Alkohol der Klasse Ethanol, Isopropanol, Benzylalkohol, Butanol, Amylalkohol oder aus einem mindestens eine derselben enthaltenden, azeotropen Gemisch besteht und geeignet ist, mindestens einen Teil des Koffeins von aktiven Zentren der Aktivkohle zu verdrängen, diese Berührung während eines solchen Zeitraums und bei einer solchen Temperatur aufrechterhalten wird, daß mindestens ein Teil des Koffeins durch das Lösungsmittel von der Aktivkohle verdrängt und in dem Lösungsmittel gelöst wird und das Koffein von dem Lösungsmittel abgetrennt wird.

2. Verfahren nach Anspruch 1, dadurch gekennzeichnet, daß die Berührung bei einer Temperatur über 100°C aufrechterhalten wird.

3. Verfahren nach Anspruch 1 und 2, dadurch gekennzeichnet, daß die Berührung unter einem Überdruck aufrechterhalten wird.

4. Verfahren nach Anspruch 1 oder 2, dadurch gekennzeichnet, daß die Berührung unter einem Druck aufrechterhalten wird, der nicht höher ist als der atmosphärische Druck.

5. Verfahren nach einem der Ansprüche 2 bis 4, dadurch gekennzeichnet, daß das Lösungsmittel Eisenessig oder ein azeotropes Gemisch ist, das Essigsäure und einen aus Butylalkohol, Isoamyl-alkohol, Toluol, n-Hexan, n-Heptan und n-Octan ausgewählten Lösungsvermittler enthält.

6. Verfahren nach einem der Ansprüche 1 bis 5, dadurch gekennzeichnet, daß die Berührung während eines Zeitraums aufrechterhalten wird, der genügt, um mindestens 75 Gew.% des Koffeins von der Aktivkohle zu verdrängen und in dem Lösungsmittel aufzulösen.

7. Verfahren nach einem der Ansprüche 1 bis 6, dadurch gekennzeichnet, daß vor dem Abtrennen des Koffeins von dem Lösungsmittel dieses von der Aktivkohle abgetrennt wird.

8. Verfahren nach einem der Ansprüche 1 bis 7, dadurch gekennzeichnet, daß das Koffein von dem Lösungsmittel durch Dampfdestillation abgetrennt wird.

9. Verfahren nach einem der Ansprüche 1 bis 8, dadurch gekennzeichnet, daß das Koffein von dem Lösungsmittel durch Verdampfen des Lösungsmittels abgetrennt wird.

Revendications

1. Procédé de récupération de caféine au départ d'un charbon activé, comprenant : la mise en contact de charbon activé sur lequel de la caféine obtenue de la décaféination d'une matière végétale est adsorbée, avec un solvant de caféine de qualité alimentaire, non toxique, comestible, liquide, qui est constitué essentiellement par un acide organique choisi parmi l'acide acétique glacial, l'acide propionique ou l'acide butyrique, ou par un alcool choisi parmi l'éthanol, l'isopropanol, l'alcool benzylique, le butanol ou l'alcool amylique, ou par un azéotrope comprenant au moins l'un de ces derniers, ce solvant étant capable de déplacer au moins une portion de la caféine depuis les sites actifs existant sur le charbon; l'entretien du contact pendant une période de temps et à une température efficaces pour que le solvant déplace au moins une portion de la caféine depuis le charbon et dissolve la caféine déplacée; et la séparation de la caféine à partir du solvant.

2. Procédé suivant la revendication 1, caractérisé en ce que le contact est entretenu à une température supérieure à 100°C.

3. Procédé suivant l'une ou l'autre des revendications 1 et 2, caractérisé en ce que le contact est entretenu à une pression supérieure à la pression atmosphérique.

4. Procédé suivant l'une ou l'autre des revendications 1 et 2, caractérisé en ce que le contact est entretenu à une pression non supérieure à la pression atmosphérique.

5. Procédé suivant l'une quelconque des revendications 2 à 4, caractérisé en ce que le solvant est l'acide acétique glacial ou un azéotrope d'acide acétique contenant un co-solvant choisi parmi l'alcool butylique, l'alcool iso-amylique, le toluène, le n-hexane, le n-heptane et le n-octane.

6. Procédé suivant l'une quelconque des revendications 1 à 5, caractérisé en ce que le contact est entretenu pendant une période de temps suffisante pour permettre un déplacement d'au moins 75 % en poids de la caféine depuis le charbon et sa mise en solution avec le solvant.

7. Procédé suivant l'une quelconque des revendications 1 à 6, caractérisé en ce que le solvant est séparé du charbon par filtration avant séparation de la caféine à partir du solvant.

8. Procédé suivant l'une quelconque des revendications 1 à 7, caractérisé en ce que la caféine est séparée du solvant par un distillation à la vapeur d'eau.

9. Procédé suivant l'une quelconque des revendications 1 à 8, caractérisé en ce que la caféine est séparée du solvant par évaporation de celui-ci.